WO2017001549A1 - Propofol emulsion for parenteral administration - Google Patents
Propofol emulsion for parenteral administration Download PDFInfo
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- WO2017001549A1 WO2017001549A1 PCT/EP2016/065279 EP2016065279W WO2017001549A1 WO 2017001549 A1 WO2017001549 A1 WO 2017001549A1 EP 2016065279 W EP2016065279 W EP 2016065279W WO 2017001549 A1 WO2017001549 A1 WO 2017001549A1
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- emulsion
- oil
- pharmaceutically acceptable
- propofol
- emulsion according
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/10—Dispersions; Emulsions
- A61K9/107—Emulsions ; Emulsion preconcentrates; Micelles
- A61K9/1075—Microemulsions or submicron emulsions; Preconcentrates or solids thereof; Micelles, e.g. made of phospholipids or block copolymers
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K31/00—Medicinal preparations containing organic active ingredients
- A61K31/045—Hydroxy compounds, e.g. alcohols; Salts thereof, e.g. alcoholates
- A61K31/05—Phenols
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/0012—Galenical forms characterised by the site of application
- A61K9/0019—Injectable compositions; Intramuscular, intravenous, arterial, subcutaneous administration; Compositions to be administered through the skin in an invasive manner
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P25/00—Drugs for disorders of the nervous system
- A61P25/20—Hypnotics; Sedatives
Definitions
- compositions for parenteral administration comprising propofol.
- the present disclosure further relates to a method for manufacturing the compositions of the disclosure as well as to the use of the compositions of the disclosure.
- Propofol (2,6-diisopropylphenol) is a short acting anaesthetic that is registered for the induction and maintenance of anaesthesia in adults and children above 3 years of age, for sedation during surgical and diagnostic measures and for sedation of ventilated patients above 16 years of age in the context of intensive care.
- Propofol offers various advantages over other agents, such as rapid onset, short duration of action, and excellent quality of recovery.
- Propofol is a highly lipophilic liquid, its lipophilicity allowing for easy permeation of the blood brain barrier, resulting in a rapid anaesthetic effect.
- propofol has a low tendency to accumulate in the body.
- the first clinical trials have been conducted with a formulation containing Cremophor EL, a polyethoxylated castor oil. This formulation has been associated with the incidence of anaphylaxis.
- cyclodextrin complexes are not an option for alpha- and beta- cyclodextrins as these show renal toxicity and are thus not suitable for parenteral application at all.
- Other cyclodextrins may only be administered in limited amounts (see “Background review for cyclodextrins used as excipients" issued by the EMEA on 20 November 2014, downloaded on 18 June 2015 from the homepage of the EMEA: http://www.ema.europa.eu/docs/en GB/document library/Report/2014/12/WC5001779 36.pdf).
- Microemulsions require the addition of large amounts of synthetic emulsifiers being less compatible than naturally occurring lecithins.
- prodrugs of propofol instead of propofol itself is hampered by the fact that pharmacokinetics are changed.
- propofol may be provided in form of an emulsion comprising low concentrations of free propofol in the aqueous phase.
- the present disclosure relates to an emulsion comprising 0.1 to 10 wt.%, preferably 1 to 5 wt.%, propofol and 5 to 25 wt.%, preferably 10 to 20 wt.%, of an oil phase based on the total weight of the emulsion, wherein the free propofol concentration in the aqueous phase is below 0.1 % of the total propofol content.
- free propofol concentration in the aqueous phase refers to the concentration of free propofol in the aqueous phase as measured by the following method:
- Propofol emulsions (aliquots of 30 ml) were dialyzed for 24 hours at 25 °C using a dialysis membrane with a cutoff molecular weight of 3500 Da (dialysis tube: Roth No. E656.1 ) versus an aqueous solution of 2.5 % glycerol.
- the concentrations of free propofol in the aqueous phase were measured by high performance liquid chromatography (e.g. using the Agilent Technologies 1200 series), using a mixture of water and acetonitrile as mobile phase at the following gradient:
- the flow rate was 1 .0 ml/min, the injection volume was 10 ⁇ , and the components of the column effluent were monitored using an ultraviolet detector at a wavelength of 275 nm. Calculations were performed by means of an external calibration with the analyte using 3-point-calibration.
- compositions according to the present disclosure are emulsions, preferably oil-in- water emulsions, i.e. the continous phase is aqueous and comprises oil droplets.
- the emulsion comprises the continous aqueous phase and preferably 5 wt.% to 25 wt.% of an oil phase based on the total weight of the emulsion. More preferably, the emulsion comprises 10 wt% to 20 wt.% of an oil phase based on the total weight of the emulsion. For example, the emulsion comprises 10 wt.% or 20 wt.% of an oil phase based on the total weight of the emulsion.
- the aqueous phase comprises water in purity suitable for parenteral administration, i.e. water for injection.
- Oil-in-water emulsions for parenteral administration have to be sterile, pyrogen-free, well tolerated, isotonic or as close as possible to isotonicity, free of particulate impurities and storage stable.
- Their pH should be as close as possible to the pH of the blood.
- oil-in-water emulsions for parenteral administration must contain only very few oil droplets larger than 5 ⁇ .
- the USP refers to this parameter as graspPFAT 5 ", which should not exceed 0.05 (compare USP 36 NF31 ⁇ 729>).
- the PFAT 5 value refers to the volume-weighted, large-diameter fat globule limits of the dispersed phase, expressed as the percentage of fat residing in globules larger than 5 ⁇ (PFAT 5 ).
- the oil phase
- the oil phase may comprise a variety of different lipids, e.g. oils, e.g. soybean oil, olive oil, fish oil, fish oil extract, safflower oil, corn oil, sunflower oil, coconut oil, palm kernel oil, rapeseed oil, medium chain triglycerides (MCT) and mixtures thereof.
- oils e.g. soybean oil, olive oil, fish oil, fish oil extract, safflower oil, corn oil, sunflower oil, coconut oil, palm kernel oil, rapeseed oil, medium chain triglycerides (MCT) and mixtures thereof.
- oils e.g. soybean oil, olive oil, fish oil, fish oil extract, safflower oil, corn oil, sunflower oil, coconut oil, palm kernel oil, rapeseed oil, medium chain triglycerides (MCT) and mixtures thereof.
- MCT medium chain triglycerides
- the oil phase comprises one or more oils selected from the group consisting of soybean oil, olive oil, fish oil, fish oil extract and MCT. More preferably, the oil phase comprises fish oil or a mixture of soybean oil, olive oil, fish oil and MCT.
- fish oil refers to “purified fish oil” and to "purified fish oil rich in omega 3 fatty acids", the latter according to the European Pharmacopoeia 6.0 comprising at least 9 wt.% of the omega-3-fatty acid docosahexaenoic acid (DHA) and at least 13 wt.% of the omega-3 fatty acid eisosapentaenoic acid (EPA) expressed as triglycerides.
- DHA docosahexaenoic acid
- EPA omega-3 fatty acid eisosapentaenoic acid
- fish oil extract refers to mixtures highly concentrated in EPA and DHA obtained e.g. from fish oil e.g. by supercritical fluid extraction and subsequent purification via e.g. chromatographic methods.
- the oil can be extracted using extraction techniques such as the one described in US6750048. Additional extraction and/or purification techniques are described in WO2001 /076715 and WO2001 /076385.
- the sum of EPA and DHA contained in these fish oil extracts is at least 500 milligram per gram of extract.
- the fish oil extract comprises EPA and DHA in esterified form, e.g. in form of triglycerides or ethyl esters.
- medium chain triglycerides refers to triglycerides of fatty acid being 6 to 12 carbon atoms in length, including caproic acid, caprylic acid, capric acid and lauric acid.
- the emulsions according to the present disclosure comprise at least one pharmaceutically acceptable emulsifier.
- emulsifier refers to compounds which stabilize the composition by reducing the interfacial tension between the oil phase and the water phase and which typically comprise at least one hydrophobic group and at least one hydrophilic group.
- These emulsifiers (which may also be referred to as surfactants) are preferably used in amounts effective to provide, optionally together with further surfactants present, a stable and even distribution of the oil phase within the aqueous phase.
- the emulsifier is selected from the group of emulsifiers that have been approved for parenteral administration.
- the at least one emulsifier is lecithin.
- lecithin refers to naturally occurring or synthetic lecithin that may be suitably refined. Suitable lecithins include, but are not limited to, lecithins derived from egg, corn or soybean or mixtures thereof. Lecithins are typically mixtures of diglycerides of fatty acids linked to the choline ester of phosphoric acid and can contain differing amounts of other compounds depending on the method of isolation. Typically, commercial lecithin is a mixture of acetone-insoluble phosphatides.
- the lecithin is obtained from egg or from seeds including soybean and corn, using methods well known in the art. Lecithin obtained from soybean is referred to herein as soy lecithin. Lecithin obtained from egg is referred to herein as egg lecithin.
- the emulsions comprise lecithin as emulsifier, more preferably the lecithin is selected from the group consisting of egg lecithin, soy lecithin, and mixtures thereof. These are commercially available, e.g. under the trade names EpikurinTM170 (soy lecithin), PL 90 or Lipoid E80 (both egg lecithin).
- the lecithin is used in an amount of 0.5 to 5 wt.%, more preferably 0.5 to 3 wt.%, most preferably 1 .0 to 2.5 wt.%.
- krill oil may be used as an emulsifier.
- Krill oil is an extract prepared from a species of antarctic krill, Euphausia superba. It has obtained GRAS (generally recognized as safe) status from the FDA and is commercially available, e.g. from Olympic Seafood (Bioriginal Europe/Asia B.V.) and Aker BioMarine Antarctic AS.
- the emulsifying properties of krill oil mainly rely on its content in phospholipids (including phosphatidylcholine, phosphatidylethanolamine and phosphatidylinositol).
- the emulsion may comprise at least one pharmaceutically acceptable antioxidant.
- An antioxidant useful in the emulsion of the disclosure may be any pharmaceutically acceptable compound having antioxidant activity, for example, the antioxidant may be selected form the group consisting of sodium metasulfite, sodium bisulfite, sodium sulfite, sodium thiosulfate, thioglycerol, thiosorbitol, thioglycolic acid, cysteine hydrochloride, n-acetly-cysteine, citric acid, alpha-tocopherol, beta-tocopherol, gamma- tocopherol, soluble forms of vitamin E, butylated hydroxyanisole (BHA), butylated hydroxytoluene (BHT), t-butylhydroquinone (TBHQ), monothioglycerol, propyl gallate, histidine, enzymes such as superoxide dismutase, catalase, selenium glutathione peroxidase,
- the at least one antioxidant is in particular selected from the group consisting of alpha- tocopherol, beta-tocopherol, gamma-tocopherol, ascorbic acid, and mixtures of two or more thereof.
- the total amount of agents with antioxidant activity is preferably in the range of from 0.01 wt.% to 0.05 wt %, more preferably from 0.01 wt.% to 0.04 wt.%, more preferably from 0.01 wt.% to 0.03 wt.%, and even more preferably from 0.015 wt.% to 0.025 wt.% based on the total weight of the emulsion.
- the tonicity agent is the tonicity agent
- the emulsion may comprise at least one pharmaceutically acceptable tonicity agent.
- Tonicity agents are used to confer tonicity.
- Suitable tonicity agents may be selected from the group consisting of sodium chloride, mannitol, lactose, dextrose, sorbitol and glycerol.
- the tonicity agent is glycerol.
- the total amount of tonicity agents is in the range of 0.1 to 10 wt.%, more preferably from 1 wt.% to 5 wt.%, more preferably from 1 wt.% to 4 wt.%, more preferably 1 wt.% to 3 wt.%, more preferably from 1 .5 wt.% to 2.8 wt.%, and even more preferably from 2.0 wt.% to 2.8 wt.% based on the total weight of the emulsion.
- the tonicity agent is glycerol
- the most preferred amount is 2.0 wt.% to 2.5 wt.% based on the total weight of the emulsion.
- the emulsion has an osmolality in the range of 305 to 420 mOsmol/kg, measured with a Vapor Pressure Osmometer, Model 5520 (Vapro TM) according to USP ⁇ 785>. pH adjustment
- the pH of the emulsion may be adjusted by adding solutions of conventionally known acids or bases such as HCI and NaOH or through the use of buffers, such as phosphate buffers.
- the final pH of the emulsion is preferably in the range of from 6 to 9, more preferably between 7 and 9.
- the pH of the emulsion according to the disclosure is adjusted using a solution of NaOH.
- the emulsion according to the disclosure may further comprise a pharmaceutically acceptable co-surfactant.
- a co-surfactant is an amphiphilic molecule, i.e. a molecule that contains both hydrophilic and lipophilic groups.
- a co-surfactant substantially accumulates with the emulsifier at the interfacial layer.
- the hydrophile-lipophile balance (HLB) number is used as a measure of the ratio of hydrophilic and lipophilic groups present in a surfactant or co-surfactant, respectively.
- HLB hydrophile-lipophile balance
- a co-surfactant with a very low HLB value is used together with a surfactant with a high HLB to modify the overall HLB of the system.
- the co- surfactant may not be capable of forming self-associated structures, like micelles, on its own.
- the co-surfactant is usually used in a lower amount than that of the emulsifier.
- the co-surfactant has the effect of further reducing the interfacial tension and increasing the fluidity of the interface.
- Co-surfactants may also adjust the curvature of the interfacial film by partitioning between the tails of the emulsifier chains, allowing greater penetration of the oil between the emulsifier tails.
- the co-surfactant is a free unsaturated fatty acid or a salt thereof, preferably an omega-9 fatty acid or a salt thereof, more preferably a monounsaturated omega-9 fatty acid or a salt thereof, more preferably oleic acid or sodium oleate.
- the total amount of the co-surfactant is preferably in the range of from 0.01 wt.% to 1 wt.%, more preferably in the range of from 0.02 wt.% to 0.5 wt.%, more preferably in the range of from 0.02 wt.% to 0.20 wt.% based on the total weight of the emulsion.
- the emulsion according to the disclosure may further comprise a pharmaceutically acceptable co-solvent.
- co-solvent refers to molecules that may increase the stability of the emulsion.
- co-solvents increase the amount of molecularly dispersed emulsifier and/or co-surfactant in the aqueous phase.
- Availability of free surfactant aids in the solubilization of hydrophobic molecules by creating pockets of hydrophobic regions within the aqueous phase.
- the co-solvent may be selected from the group consisting of ethanol, propylene glycol and polyethylen glycol.
- the co-solvent is a polyalkylene glycol or an alkylene glycol, preferably polyethylen glycol or polypropylen glycol, more preferably polyethylene glycol (PEG).
- PEG polyethylene glycol
- the PEG preferably has a mean molecular weight in the range of from 100 to 20000 Da, more preferably in the range of from 200 to 1000 Da, more preferably in the range of from 300 to 600 Da, most preferably around 400 Da.
- the co-solvent is selected from the group consisting of PEG 200, PEG 300, PEG 400, PEG 600, PEG, 1000, PEG 1450, PEG 4000, PEG 6000, PEG 8000 and PEG 20000. Most preferably, the co-solvent is PEG 400.
- the total amount of co-solvents ranges from 0.1 wt% to 2.0 wt.%, more preferably from 0.25 wt.% to 1 .75 wt.%, more preferably from 0.50 wt.% to 1 .50 wt.%, more preferably from 0.70 wt.% to 1 .40 wt.%, more preferably from 0.80 wt.% to 1 .30 wt.%, and even more preferably from 0.90 wt.% to 1 .20 wt.% based on the total weight of the emulsion.
- the droplet size ranges from 0.1 wt% to 2.0 wt.%, more preferably from 0.25 wt.% to 1 .75 wt.%, more preferably from 0.50 wt.% to 1 .50 wt.%, more preferably from 0.70 wt.% to 1 .40 wt.%, more preferably from 0.80 wt.% to 1 .
- the continous phase is aqueous and comprises oil droplets. These oil droplets are stabilized within the aqueous phase by at least one emulsifier and optionally further additives.
- the size of the oil droplets depends on the qualitative and quantitative composition of the emulsion and its preparation.
- the oil droplets of the emulsion herein preferably have a mean diameter of 130 to 300 nm when measured directly upon sterilization using an LS 13 320 Laser Diffraction Particle Size Analyser (Beckman Coulter) according to USP ⁇ 729>.
- the present disclosure also relates to a method for preparing an emulsion for parenteral administration and to an emulsion obtained or obtainable by said method, wherein the method comprises
- an aqueous phase comprising water for injection and optionally a pharmaceutically acceptable tonicity agent and/or an agent for pH adjustment and/or a pharmaceutically acceptable co-surfactant and/or a pharmaceutically acceptable co-solvent
- step c) forming a pre-emulsion by mixing the oil phase provided in step a) with the aqueous phase provided in step b);
- step c) forming the emulsion by high-pressure homogenizing the pre-emulsion obtained in step c) and
- step e) sterilizing the emulsion obtained in step d), wherein optionally either in step a) or in step b) a pharmaceutically acceptable emulsifier is added.
- any of the optional further components of the emulsion may be added in any of the steps a), b), c) or d) or in one or more additional steps.
- Step a) is preferably carried out by mixing one or more lipids, propofol and optionally a pharmaceutically acceptable antioxidant and/or co-surfactant. This step is preferably carried out at a temperature of 55 to 65 °C, wherein during this step the temperature may be varied or held essentially constant for a maximum 30 minutes until a homogeneous and clear phase is obtained.
- step a) further additives may be added.
- the at least one pharmaceutically acceptable emulsifier - depending on its nature - may be added either in step a) or in step b).
- Step b) is preferably carried providing water for injection and optionally adding a pharmaceutically acceptable tonicity agent and/or co-surfactant.
- the aqueous phase is then heated to a temperature of 55 to 65 °C, preferably for a time of 1 minute to 1 hour, more preferably from 5 to 30 minutes, more preferably from 5 to 15 minutes.
- step b) further comprises adjusting the pH to values between 7 and 10, preferably to a pH between 8 and 9, preferably by adding a solution of NaOH.
- step b) further additives may be added.
- the at least one pharmaceutically acceptable emulsifier - depending on its nature - may be added either in step a) or in step b).
- the method further comprises mixing the oil phase provided in step a) with the aqueous phase provided in step b) thereby forming a pre-emulsion.
- the mixing may be carried out by any method known to those skilled in the art.
- the mixing is carried out using a high shear mixer.
- the oil phase is added to the aqueous phase or vice-versa at a temperature in the range of from 55 to 65 °C.
- the oil phase is added to the aqueous phase or vice-versa at a pressure such as as under nitrogen pressure, in the range of from 0.20 to 0.80 bar, more preferably from 0.2 to 0.4 bar.
- a pressure such as as under nitrogen pressure, in the range of from 0.20 to 0.80 bar, more preferably from 0.2 to 0.4 bar.
- the pressure may be varied or held essentially constant.
- the mixture is stirred for a time in the range of from 1 minute to 1 hour, preferably from 10 to 30 minutes.
- the temperature may be varied or held essentially constant.
- the pH of the pre-emulsion is adjusted to a pH in the range of from 8 to 10, in particular by adding sodium hydroxide, if necessary.
- the method further comprises the homogenization of the pre-emulsion obtained in step c).
- This homogenization may be carried out by any suitable method known to those skilled in the art.
- the mixture is homogenized at a temperature in the range of from 40 to 60 °C, preferably from 45 to 55 °C.
- the pre-emulsion is homogenized at a pressure in the range of from 400 to 600 bar, more preferably from 450 to 550 bar. During this step the pressure may be varied or held essentially constant.
- the homogenization is carried out using a high pressure homogenizer or a microfluidizer.
- the method further comprises the sterilization of the emulsion obtained in step d) to ensure its suitability for parenteral administration.
- the sterilization may be carried out by any suitable method known to those skilled in the art.
- the sterilization is carried out by autoclaving, preferably at a temperature in the range of from 1 19 to 122 °C, more preferably at a temperature around 121 °C, preferably for a time in the range of from 1 minute to 30 minutes, preferably of from 10 minutes to 15 minutes.
- Route of administration preferably at a temperature in the range of from 1 19 to 122 °C, more preferably at a temperature around 121 °C, preferably for a time in the range of from 1 minute to 30 minutes, preferably of from 10 minutes to 15 minutes.
- compositions according to the present disclosure are adapted for parenteral administration, i.e. for a route of administration "other than via the gastrointestinal tract".
- the compositions according to the present disclosure are administered intravenously.
- the present disclosure includes inter alia the following aspects:
- the present disclosure relates to an emulsion for parenteral administration comprising 0.1 to 10 wt.%, preferably 1 to 5 wt.%, propofol and 5 to 25 wt.%, preferably 10 to 20 wt.%, of an oil phase based on the total weight of the emulsion, wherein the free propofol concentration in the aqueous phase is below 0.1 % of the total propofol content.
- the present disclosure relates to an emulsion according to aspect 1 , wherein the oil phase comprises fish oil, fish oil extract, soybean oil, olive oil, medium chain triglycerides (MCT) or mixtures thereof.
- the present disclosure relates to an emulsion according to aspect 1 or 2, wherein the oil phase comprises fish oil.
- the present disclosure relates to an emulsion according to any of the preceding aspects, wherein the oil phase comprises fish oil, soybean oil, olive oil and medium chain triglycerides (MCT).
- the oil phase comprises fish oil, soybean oil, olive oil and medium chain triglycerides (MCT).
- the present disclosure relates to an emulsion according any of the preceding aspects comprising a pharmaceutically acceptable emulsifier, preferably egg lecithin or krill oil.
- the present disclosure relates to an emulsion according to any of the preceding aspects comprising a pharmaceutically acceptable tonicity agent, preferably glycerol.
- the present disclosure relates to an emulsion according to any of the preceding aspects comprising a pharmaceutically acceptable antioxidant, preferably alpha-tocopherol or a mixture of alpha-, beta- and gamma-tocopherol.
- a pharmaceutically acceptable antioxidant preferably alpha-tocopherol or a mixture of alpha-, beta- and gamma-tocopherol.
- the present disclosure relates to an emulsion according to any of the preceding aspects comprising a pharmaceutically acceptable co-surfactant, preferably oleic acid or sodium oleate.
- the present disclosure relates to an emulsion according to any of the preceding aspects comprising a pharmaceutically acceptable co-solvent, preferably polyethylen glycol (PEG).
- a pharmaceutically acceptable co-solvent preferably polyethylen glycol (PEG).
- the present disclosure relates to an emulsion according to any of the preceding aspects comprising an agent for pH adjustment, preferably NaOH.
- the present disclosure relates to an emulsion according to any of the preceding aspects, wherein the emulsion is an oil-in-water emulsion and wherein the oil droplets dispersed in the aqueous phase have a mean diameter of 130 to 300 nm.
- the present disclosure relates to an emulsion according to any of the preceding aspect for use in anaesthesia or sedation.
- the present disclosure relates to the use according to aspect 12 in patients suffering from disturbed liver function, blood coagulation disorder or inflammatory disease.
- the present disclosure relates to the use according to aspects 12 and 13, wherein the administration of the emulsion causes reduced pain on injection.
- the present disclosure relates to a method for manufacturing the emulsion according to any of the aspects 1 to 15, comprising
- an oil phase comprising one or more oils according to any of the aspects 2 to 4, propofol and optionally at least one pharmaceutically acceptable antioxidant and/or a pharmaceutically acceptable co-surfactant;
- an aqueous phase comprising water for injection and optionally a pharmaceutically acceptable tonicity agent and/or an agent for pH adjustment and/or a pharmaceutically acceptable co-surfactant and/or a pharmaceutically acceptable co-solvent;
- step c) forming a pre-emulsion by mixing the oil phase provided in step a) with the aqueous phase provided in step b);
- step c) forming the emulsion by high-pressure homogenizing the pre-emulsion obtained in step c) and
- step d) sterilizing the emulsion obtained in step d), wherein optionally either in step a) or in step b) a pharmaceutically acceptable emulsifier is added.
- Emulsion for parenteral administration comprising 0.1 to 10 wt.%, preferably 1 to 5 wt.%, propofol and 5 to 25 wt.%, preferably 10 to 20 wt.%, of an oil phase based on the total weight of the emulsion, wherein the free propofol concentration in the aqueous phase is below 0.1 % of the total propofol content.
- Emulsion according to embodiment 1 comprising 10 wt.% of an oil phase and 1 wt.% Propofol based on the total weight of the emulsion.
- Emulsion according to embodiment 1 comprising 10 wt.% of an oil phase and 2 wt.% propofol based on the total weight of the emulsion.
- Emulsion according to embodiment 1 comprising 10 wt.% of an oil phase and 5 wt.% propofol based on the total weight of the emulsion.
- Emulsion according to embodiment 1 comprising 20 wt.% of an oil phase and 1 wt.% propofol based on the total weight of the emulsion.
- Emulsion according to embodiment 1 comprising 20 wt.% of an oil phase and 2 wt.% propofol based on the total weight of the emulsion.
- Emulsion according to embodiment 1 comprising 20 wt.% of an oil phase and 5 wt.% propofol based on the total weight of the emulsion.
- Emulsion according to any of the preceding embodiments wherein the oil phase comprises fish oil extract. 1 1 ) Emulsion according to any of the preceding embodiments, wherein the oil phase comprises fish oil, olive oil, soybean oil and medium chain triglycerides (MCT). 12) Emulsion according to any of the preceding embodiments comprising a pharmaceutically acceptable emulsifier, preferably egg lecithin or krill oil. 13) Emulsion according to any of the preceding embodiments comprising a pharmaceutically acceptable tonicity agent, preferably glycerol.
- MCT medium chain triglycerides
- Emulsion according to any of the preceding embodiments comprising a pharmaceutically acceptable antioxidant, preferably alpha-tocopherol or a mixture of alpha-, beta- and gamma-tocopherol.
- a pharmaceutically acceptable antioxidant preferably alpha-tocopherol or a mixture of alpha-, beta- and gamma-tocopherol.
- Emulsion according to any of the preceding embodiments comprising a pharmaceutically acceptable co-surfactant, preferably oleic acid or sodium oleate.
- a pharmaceutically acceptable co-solvent preferably polyethylen glycol (PEG).
- Emulsion according to any of the preceding embodiments comprising an agent for pH adjustment, preferably NaOH.
- Emulsion according to any of the preceding embodiments wherein the emulsion is an oil-in-water emulsion and wherein the oil droplets dispersed in the aqueous phase have a mean diameter of 130 to 300 nm.
- Emulsion according to any of the preceding embodiments for use in anaesthesia or sedation.
- Method for preparing an emulsion according to any of the embodiments 1 to 18 comprising a) Providing an oil phase comprising one or more oils according to any of embodiments 8 to 1 1 , propofol and optionally a pharmaceutically acceptable co-surfactant and or a pharmaceutically acceptable antioxidant, b) Providing an aqueous phase comprising water for injection, and optionally a pharmaceutically acceptable tonicity agent and/or an agent for pH- adjustment and/or a pharmaceutically acceptable co-solvent,
- step c) Forming a pre-emulsion by mixing the oil phase obtained in step a) with the aqueous phase obtained in step b),
- step c) Forming an emulsion by high pressure homogenizing the pre-emulsion obtained in step c),
- step d) Sterilizing the emulsion obtained in step d), wherein optionally either in step a) or in step b) a pharmaceutically acceptable emulsifier is added.
- the emulsion was prepared from the ingredients listed in table 1 .
- the oil phase was prepared by mixing fish oil and Propofol. The mixture was heated to 60 °C.
- the aqueous phase was prepared by mixing water, glycerol and sodium oleate. The mixture was heated to 60 °C, and then egg lecithin was added.
- the pre-emulsion was formed by adding the oil phase to the aqueous phase under continous agitation using a high shear mixer (Ultra Turrax T50) at a temperature of 60 °C.
- a high shear mixer Ultra Turrax T50
- the emulsion was formed by passing the pre-emulsion six times through a Niro Soavi Twin Panda 600 homogenizer at 500 bar at a temperature of 50 °C.
- the pH was adjusted to 8.0 to 9.0.
- the oil droplets of the emulsion according to example 1 had a mean diameter of 145 nm when measured directly upon sterilization using an LS 13 320 Laser Diffraction Particle Size Analyser (Beckman Coulter) according to USP ⁇ 729>.
- the emulsion according to example 1 is stable for at least 26 weeks.
- the emulsions were prepared from the ingredients listed in table 3.
- the oil phases were prepared by mixing fish oil and propofol. The mixture was heated to 60 °C.
- the aqueous phases were prepared by mixing water, glycerol and sodium oleate. The mixture was heated to 60 °C, and then egg lecithin was added.
- the pre-emulsions were formed by adding the oil phases to the aqueous phases under continous agitation using a high shear mixer (Ultra Turrax T50) at a temperature of 60 °C.
- a high shear mixer Ultra Turrax T50
- the emulsions were formed by passing the pre-emulsions six times through a Niro Soavi Twin Panda 600 homogenizer at 500 bar at a temperature of 50 °C.
- the pH was adjusted to 8.0 to 9.0.
- the oil droplets of the emulsion according to example 2a had a mean diameter of 177 nm when measured directly upon sterilization.
- the oil doplets of the emulsion according to example 2b had a mean diameter of 155 nm when measured directly upon sterilization using an LS 13 320 Laser Diffraction Particle Size Analyser (Beckman Coulter) according to USP ⁇ 729>.
- the emulsions according to examples 2a) and 2b) are stable for at least 12 months.
- the emulsions were prepared from the ingredients listed in table 5.
- the oil phases were prepared by mixing soybean oil, medium chain triglycerides, olive oil, fish oil, propofol and alpha-tocopherol. The mixture was heated to 60 °C.
- the aqueous phases were prepared by mixing water, glycerol and sodium oleate. The mixture was heated to 60 °C, and then egg lecithin was added.
- the pre-emulsions were formed by adding the oil phases to the aqueous phases under continous agitation using a high shear mixer (Ultra Turrax T50) at a temperature of 60 °C.
- a high shear mixer Ultra Turrax T50
- the emulsions were formed by passing the pre-emulsion six times through a Niro Soavi Twin Panda 600 homogenizer at 500 bar at a temperature of 50 °C.
- the pH was adjusted to 8.0 to 9.0.
- the oil droplets of the emulsion according to example 3 had a mean diameter of 163 nm (3a), 149 nm (3b), 289 nm (3c) and 181 nm (3d) respectively when measured directly upon sterilization using an LS 13 320 Laser Diffraction Particle Size Analyser (Beckman Coulter) according to USP ⁇ 729>.
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Abstract
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Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
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CA2991084A CA2991084A1 (en) | 2015-07-01 | 2016-06-30 | Propofol emulsion for parenteral administration |
MX2017016998A MX2017016998A (en) | 2015-07-01 | 2016-06-30 | Propofol emulsion for parenteral administration. |
CN201680038788.2A CN107708669B (en) | 2015-07-01 | 2016-06-30 | Propofol emulsions for parenteral administration |
US15/740,923 US20180185280A1 (en) | 2015-07-01 | 2016-06-30 | Propofol emulsion for parenteral administration |
EP16734332.6A EP3316859B1 (en) | 2015-07-01 | 2016-06-30 | Propofol emulsion for parenteral administration |
ZA2017/08086A ZA201708086B (en) | 2015-07-01 | 2017-11-28 | Propofol emulsion for parenteral administration |
HK18113515.9A HK1254431A1 (en) | 2015-07-01 | 2018-10-22 | Propofol emulsion for parenteral administration |
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EP15174744 | 2015-07-01 | ||
EP15174744.1 | 2015-07-01 |
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PCT/EP2016/065279 WO2017001549A1 (en) | 2015-07-01 | 2016-06-30 | Propofol emulsion for parenteral administration |
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US (1) | US20180185280A1 (en) |
EP (1) | EP3316859B1 (en) |
CN (1) | CN107708669B (en) |
CA (1) | CA2991084A1 (en) |
HK (1) | HK1254431A1 (en) |
MX (1) | MX2017016998A (en) |
WO (1) | WO2017001549A1 (en) |
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CA3155749A1 (en) * | 2019-12-20 | 2021-06-24 | Fresenius Kabi Austria Gmbh | Method for producing oil-in-water emulsions |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
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US20040225022A1 (en) * | 2003-05-09 | 2004-11-11 | Desai Neil P. | Propofol formulation containing reduced oil and surfactants |
WO2007052288A2 (en) * | 2005-08-05 | 2007-05-10 | Bharat Serums & Vaccines Ltd. | Intravenous propofol emulsion compositions having preservative efficacy |
Family Cites Families (3)
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CN1965806A (en) * | 2006-11-09 | 2007-05-23 | 华瑞制药有限公司 | Fat emulsion injection liquid containing soybean oil, medium chain triglyceride, olive oil and fish oil and method for preparing the same |
CN104288130A (en) * | 2013-07-16 | 2015-01-21 | 天津迈迪瑞康生物医药科技有限公司 | A propofol composition used for injection, a preparing method thereof and uses of the propofol composition |
US20160228384A1 (en) * | 2015-02-05 | 2016-08-11 | Nanomedex, Llc | Emulsion containing two oils and stabilizers |
-
2016
- 2016-06-30 US US15/740,923 patent/US20180185280A1/en not_active Abandoned
- 2016-06-30 MX MX2017016998A patent/MX2017016998A/en active IP Right Grant
- 2016-06-30 WO PCT/EP2016/065279 patent/WO2017001549A1/en active Application Filing
- 2016-06-30 CN CN201680038788.2A patent/CN107708669B/en active Active
- 2016-06-30 EP EP16734332.6A patent/EP3316859B1/en active Active
- 2016-06-30 CA CA2991084A patent/CA2991084A1/en not_active Abandoned
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2017
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Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20040225022A1 (en) * | 2003-05-09 | 2004-11-11 | Desai Neil P. | Propofol formulation containing reduced oil and surfactants |
WO2007052288A2 (en) * | 2005-08-05 | 2007-05-10 | Bharat Serums & Vaccines Ltd. | Intravenous propofol emulsion compositions having preservative efficacy |
Non-Patent Citations (1)
Title |
---|
WEIHUI CAI ET AL: "A propofol microemulsion with low free propofol in the aqueous phase: Formulation, physicochemical characterization, stability and pharmacokinetics", INTERNATIONAL JOURNAL OF PHARMACEUTICS, vol. 436, no. 1-2, 1 October 2012 (2012-10-01), pages 536 - 544, XP055208261, ISSN: 0378-5173, DOI: 10.1016/j.ijpharm.2012.07.008 * |
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CN107708669A (en) | 2018-02-16 |
US20180185280A1 (en) | 2018-07-05 |
ZA201708086B (en) | 2020-02-26 |
HK1254431A1 (en) | 2019-07-19 |
MX2017016998A (en) | 2018-04-13 |
EP3316859B1 (en) | 2020-03-11 |
EP3316859A1 (en) | 2018-05-09 |
CA2991084A1 (en) | 2017-01-05 |
CN107708669B (en) | 2021-01-29 |
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